US4606677A - Device for introducing dosed quantities of pulverized solid materials into a carrier gas stream - Google Patents
Device for introducing dosed quantities of pulverized solid materials into a carrier gas stream Download PDFInfo
- Publication number
- US4606677A US4606677A US06/550,565 US55056583A US4606677A US 4606677 A US4606677 A US 4606677A US 55056583 A US55056583 A US 55056583A US 4606677 A US4606677 A US 4606677A
- Authority
- US
- United States
- Prior art keywords
- dosing device
- housing
- sleeve
- sleeve means
- carrier gas
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000012159 carrier gas Substances 0.000 title claims abstract description 24
- 239000011343 solid material Substances 0.000 title abstract description 6
- 239000000463 material Substances 0.000 claims abstract description 27
- 239000012530 fluid Substances 0.000 claims abstract description 5
- 238000007789 sealing Methods 0.000 claims description 3
- 229910052721 tungsten Inorganic materials 0.000 claims description 3
- 239000010937 tungsten Substances 0.000 claims description 3
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 claims description 2
- 239000002184 metal Substances 0.000 abstract description 3
- 229910052751 metal Inorganic materials 0.000 abstract description 3
- 238000007670 refining Methods 0.000 abstract description 3
- 239000004449 solid propellant Substances 0.000 abstract description 3
- 230000008901 benefit Effects 0.000 description 5
- 230000009471 action Effects 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 239000011802 pulverized particle Substances 0.000 description 3
- 230000008859 change Effects 0.000 description 2
- 239000002817 coal dust Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000000063 preceeding effect Effects 0.000 description 2
- 230000000717 retained effect Effects 0.000 description 2
- 229910000906 Bronze Inorganic materials 0.000 description 1
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 230000004323 axial length Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000010974 bronze Substances 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- KUNSUQLRTQLHQQ-UHFFFAOYSA-N copper tin Chemical compound [Cu].[Sn] KUNSUQLRTQLHQQ-UHFFFAOYSA-N 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 229910003460 diamond Inorganic materials 0.000 description 1
- 239000010432 diamond Substances 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000003077 lignite Substances 0.000 description 1
- 238000003754 machining Methods 0.000 description 1
- 230000000873 masking effect Effects 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000012254 powdered material Substances 0.000 description 1
- 230000002028 premature Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 150000003657 tungsten Chemical class 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G53/00—Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
- B65G53/34—Details
- B65G53/40—Feeding or discharging devices
- B65G53/46—Gates or sluices, e.g. rotary wheels
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B5/00—Making pig-iron in the blast furnace
- C21B5/001—Injecting additional fuel or reducing agents
- C21B5/003—Injection of pulverulent coal
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K3/00—Feeding or distributing of lump or pulverulent fuel to combustion apparatus
- F23K3/02—Pneumatic feeding arrangements, i.e. by air blast
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01F—MEASURING VOLUME, VOLUME FLOW, MASS FLOW OR LIQUID LEVEL; METERING BY VOLUME
- G01F11/00—Apparatus requiring external operation adapted at each repeated and identical operation to measure and separate a predetermined volume of fluid or fluent solid material from a supply or container, without regard to weight, and to deliver it
- G01F11/10—Apparatus requiring external operation adapted at each repeated and identical operation to measure and separate a predetermined volume of fluid or fluent solid material from a supply or container, without regard to weight, and to deliver it with measuring chambers moved during operation
- G01F11/12—Apparatus requiring external operation adapted at each repeated and identical operation to measure and separate a predetermined volume of fluid or fluent solid material from a supply or container, without regard to weight, and to deliver it with measuring chambers moved during operation of the valve type, i.e. the separating being effected by fluid-tight or powder-tight movements
- G01F11/20—Apparatus requiring external operation adapted at each repeated and identical operation to measure and separate a predetermined volume of fluid or fluent solid material from a supply or container, without regard to weight, and to deliver it with measuring chambers moved during operation of the valve type, i.e. the separating being effected by fluid-tight or powder-tight movements wherein the measuring chamber rotates or oscillates
- G01F11/24—Apparatus requiring external operation adapted at each repeated and identical operation to measure and separate a predetermined volume of fluid or fluent solid material from a supply or container, without regard to weight, and to deliver it with measuring chambers moved during operation of the valve type, i.e. the separating being effected by fluid-tight or powder-tight movements wherein the measuring chamber rotates or oscillates for fluent solid material
Definitions
- the present invention relates to an apparatus for introducing measured or dosed quantities of pulverized or pulverulent materials into a carrier gas stream.
- This invention is particularly applicable to the operation of injecting solid fuels into a shaft furnace during a metal refining process.
- European Patent Application No. 0043606 describes a pneumatic transport device for pulverulent materials, particularly coal and/or lignite dust.
- a pneumatic current or carrier gas stream is formed by the introduction or entrainment of pulverized particles (i.e., coal dust) into a current of pressurized air, whereby the finely dispersed particles are propelled therethrough.
- the well know prior art method for effecting this carrier gas stream involves a honeycomb-type rotor having plural chamber means.
- a typical prior art pneumatic transport device comprises, then, a cylindrical rotor peripherally provided with plural vanes which define individual and corresponding compartments or cells.
- This rotor will rotate within a housing about its longitudinal axis in a hermetic fashion, so that the pulverized material fed in from the top is conveyed downwardly via the compartments or cells into a current of compressed air, the compressed air serving as a propulsion fluid or carrier gas.
- This carrier gas thus carries or entrains the pulverized material subsequent to delivery by the compartment or cells.
- This well known type of dosing apparatus has certain serious deficiencies and problems.
- One such problem involves the leakage of very fine particles of the pulverulent material from the cells or chambers into and along both the rotor shaft and rotor bearings.
- these extremely fine particles easily migrate into virtually every area of the dosing mechanism including the small circular interstice located between the rotor shaft and the internal surface of the bearing. Although very small, this interstice is necessary in order to avoid undesirable friction.
- a novel device for the introduction of measured or dosed quantities of pulverized solid materials into a pneumatic propulsion fluid or carrier gas which prevents the aforementioned undesirable leakage.
- the present invention comprises a preferably cylindrical housing partially traversed in the axial direction by a pressurized fluid or carrier gas.
- the housing also has a side or radial aperture or opening which communicates with a tank containing pulverized solid material. The pressure in the tank should be above that of the carrier gas.
- the housing further contains two coaxial sleeves defined as an inner sleeve and an outer sleeve.
- the inner sleeve has an axial bore which provides passage therethrough to the carrier gas. At least one of the two sleeves is capable of rotating about its longitudinal axis and is connected for this purpose to a suitable device for imparting rotation.
- Each of the sleeves is further provided with a slot positioned so as to correspond with each other and with the side or radial aperture on the housing.
- the slots are permitted to meet and overlap each other as the rotatable sleeve rotates about its axis.
- the slots in both sleeves are respectively identical in shape and thereby complimentary.
- the respective overlapping and identical slots on the inner and outer sleeves thus define a passage of varying size (depending on the position of the rotating sleeve). This passage allows pulverized material in the tank to pass through the carrier gas stream which flows through the inner sleeve.
- the inner sleeve is movable (rotatable) and the outer sleeve is integral or attached to the housing while in a second embodiment, the inner sleeve is fixed and the outer sleeve is movable.
- This second embodiment offers an advantage over the first embodiment by reducing the risk of forming a build-up or "bridge" as discussed and defined in more detail hereinafter.
- the length of the two sleeves are approximately equal to the diameter of the side aperture of the housing.
- An annular friction ring is provided between the housing and the annular front surface of the movable sleeve.
- the movable sleeve is subjected to axial force provided by a spring means which acts to keep the sleeve in contact with the ring.
- the spring should be provided with adjustable tensioning means.
- the outer diameter of the outer sleeve is preferably less than the internal diameter of the cylindrical housing in order to define an annular space between the outer sleeve and the housing and to reduce the risk of seizing.
- FIG. 1 is a cross sectional elevation view of a first embodiment of a dosing device in accordance with the present invention.
- FIG. 2 is a cross sectional elevation view of a second embodiment of a dosing device in accordance with the present invention.
- FIG. 3a is a cross sectional elevation view of the dosing device of FIGS. 1 and 2, showing two sleeves in an open position.
- FIG. 3b is a cross sectional elevation view of the dosing device of FIG. 3a showing the two sleeves in a partially open position.
- FIG. 3c is a cross sectional elevation view of the dosing device of FIG. 3a showing the two sleeves in a partially closed position.
- FIG. 3d is a cross sectional elevation view of the dosing device of FIG. 3a showing the two sleeves in a closed position.
- FIGS. 4a, 4b and 4c are schematic views of cooperating slots in different positions having a first configuration.
- FIGS. 5a, 5b and 5c are schematic views of cooperating slots in different positions having a second configuration.
- FIGS. 6a, 6b and 6c are schematic views of cooperating slots in different positions having a third configuration.
- FIGS. 7a, 7b and 7c are schematic views of cooperating slots in different postions having a fourth configuration.
- FIG. 8 is a cross sectional elevation view of a third embodiment of a dosing device in accordance with the present invention.
- FIG. 9 is a cross sectional view along the line 9--9 in FIG. 8 and in accordance with the present invention.
- the dosing device consists of a cylindrical housing 10 which is enclosed at either end via securing flange 12 and a front plate 14.
- the housing 10 contains therein, two coaxial cylindrical sleeves 16 and 18 defined as an inner sleeve 16 and an outer sleeve 18.
- the outer sleeve 18 is fixed in position and integral with the front plate 14 while the inner sleeve 16 can freely rotate about the longtitudinal axis O.
- Running longitudinally along the inside center of inner sleeve 16 is axial bore 20 which communicates with a pneumatic transport pipe or carrier gas pipe 22.
- the housing 10 also has two lateral pipes 24 and 26, the pipe 24 communicating with a tank containing pulverized solid materials and the pipe 26 being connected to a source of compressed air which acts to convey the pulverized materials through the pipe 22.
- the pipe 26 is in direct communication via annular chamber 28 with the axial bore 20 of the inner sleeve 16.
- the two sleeves 16 and 18 are each provided with lateral or radial slots 30 and 32 respectively. These slots are positioned at a place corresponding to the point where the pulverized material exits from pipe 24. Thus, these slots define a passage between the pipe 24 and the axial bore 20 having a size which will be variable according to the angular position occupied by the movable or rotatable sleeve 16.
- FIGS. 3a through 3d are cross sections through the slots 30 and 32 which show different angular positions for the inner movable sleeve 16.
- the sleeve 16 has been positioned such that the slots 30 and 32 are in full alignment thereby defining a passage between the pipe 24 and bore 20 of maximum obtainable width.
- a rotation of the sleeve 16 will gradually reduce the cross section of the opening or passage between the pipe 24 and the axial bore 20.
- this passage narrows to a minimum width.
- the device completely closes.
- a drive shaft 34 is provided at the end opposite the discharge pipe 22.
- the shaft 34 is mounted in the housing 10 with the aid of a sealing ring 38, leakage of compressed air thus being prevented therefrom.
- This drive shaft 34 is made connected for rotation with the movable sleeve 16 by means, for example, of two diametrically opposed grips 40 which engage corresponding grooves in the front of the sleeve 16.
- the drive shaft 34 is connected by a sleeve member 42 to a stepping motor (not shown).
- One prototype of the present invention has utilized a motor which applied an electrical impulse to produce a rotation of 0.36° at a speed of 1-2 rpm.
- the compressed air or carrier gas coming from the pipe 26 passes through the annular chamber 28, and into and through the internal axial bore 20 towards the pneumatic pipe 22.
- the compressed gas carries along with it the pulverized material (i.e., coal dust) introduced via the calibrated aperture defined by the interaction of the slots 30 and 32.
- the material is delivered through the slots, in part, because of a difference between the higher pressure in the tank containing the pulverized solids (not shown in the drawing) and the lower pressure of the air in the bore 20.
- the major novel improvement achieved by the dosing device of the present invention essentially consists of the limited number of moving parts.
- the change in the rate of delivery of pulverized material was brought about by altering the rotation speed of the chamber.
- the output of pulverized material of the present invention in the device can be adjusted simply by modifying the angular position occupied by the movable sleeve. It should be noted in fact, that as long as the rate of delivery is constant there is no component in motion at all; since the movable sleeve remains stationary, whereas the prior art device required constant rotation of the honeycomb-type chamber.
- the inner sleeve 16' is fixed in position and integral with the front plate 14, while the inner socket 18' is movable and connected for this purpose to the driving shaft 34 in the same manner as in the embodiment shown in FIG. 1.
- the two slots 30' and 32' provided in the sockets 16' and 18' again define the cross section of the passage through which the pulverized material may flow.
- the device as shown in FIG. 2 does in fact offer a certain advantage over the structure of the first embodiment owing to the fact tht outer sleeve 18' is movable as opposed to the inner sleeve 16. It appears that the pulverized material which is supplied under pressure through pipe 24 tends to form a build-up or "bridge" around the slot 32 or 32' of the sleeve 18 or 18'. This "bridge” will obviously decrease the amount of material passing down through to the carrier gas. In the second embodiment where the sleeve 18' is the movable element, there is a far lesser risk of creating such an undesirable "bridge".
- FIGS. 4, 5, 6 and 7, slots of different shapes and in various positions are shown in plan view as seen looking down through the aperture 24.
- the slots are shaped as elongated ovals 30 and 32 which, in the position illustrated in FIG. 4a, only overlap to a very small extent, thus defining a flow passage of circular cross section, the width of the passage for the material thus being at its minimum.
- a rotation of the movable socket 30 or 32 will increase the cross section of the aperture, as shown in FIG. 4b, with the cross section of the flow passage reaching its maximum size in the position shown in FIG. 4c wherein the two slots 30 and 32 are in full alignment.
- FIGS. 5, 6 and 7 the positions shown in FIGS. 4a, 4b and 4c respectively are retained, but now the slots have alternative shapes.
- the set of slots in FIGS. 5a to 5c are wider (more rectangular) than the set of slots in FIGS. 4a to 4c and allow a greater delivery rate of pulverized material.
- FIGS. 6 and 7 are specially characterized by the fact that the adjustment of the cross section of the aperture is effected both in the direction of its length and in the direction of its width. This offers the advantage that the cross section is more quickly modified. Also, another advantage is that the movable socket need not perform as great a rotation for a given modification. The modification in the width of the cross section may also help to reduce the risk of the formation of a "bridge" as described earlier. As shown in FIGS. 6a-6c, the slots have an arrow shape while FIGS. 7a-7c disclose slots having a triangular shape.
- the interior of the housing 10 contains two dosing sleeves 44 and 46 having a similar structure to the dosing sleeves described earlier.
- the sleeve 44 is fixed in position and integral with the housing 10, while the sleeve 46 is movable or rotatable about the longitudinal axis O.
- Sleeve 46 is fixed to and forms the front portion of a rotatable cylindrical body 48 capable of sliding longitudinally in a longitudinal bore provided in the housing 10.
- the compressed air is supplied from conduit 26 and via both an annular chamber 50 located in the body 48 and the hollow central part of the chamber, to a mixing chamber 52 inside the inner sleeve 44.
- the mixing chamber 52 extends along the longitudinal axis of the housing 10 towards a pneumatic transport pipe (not shown). It should be understood that alternatively, the sleeve 44 may be movable while the sleeve 46 is fixed, as in the embodiment of FIG. 2.
- the two sleeves 44 and 46 are provided with dosing slots 54, 56 (see also FIG. 9) respectively.
- the dosing slots 54, 56 are actuated (i.e., relatively adjusted to form passages of varying size) by the rotation of the movable sleeve about the axis O as already described in detail with reference to the preceding figures.
- the pulverized material as shown in the left-hand portion of the diagrams, might find its way in between the movable sleeve and the inner surface of the housing and between the inner surface of the movable sleeve and the outer surface of the fixed sleeve. If the powdered material was allowed in those areas, the risk of seizing would increase.
- the pulverized material can only penetrate, at the most, the surface area between the two sleeves. Because that surface area is very limited in size and despite the presence of a small gap or clearance therebetween, the risk of seizing is greatly reduced. Note that the gap or clearance between the two sleeves presents no problem (i.e., hermeticity is ensured) due to a friction ring 58, which may be made, for example, of an alloy of teflon and bronze, and which in the FIG. 8 embodiment is positioned around the fixed sleeve 44 between the housing 10 and the end of the movable sleeve 46. This movable sleeve 46 is held against the ring 58 by the action of a spring 60.
- a friction ring 58 which may be made, for example, of an alloy of teflon and bronze
- the outer diameter of the outer sleeve 46 is less than the internal diameter of a part of the housing 10.
- an annular chamber 45 is defined between the outer sleeve and the housing which further reduces the risk of seizing by allowing the pulverized material a circulating path.
- the function of elastically holding the sleeve 46 against the ring 58 is performed by a spring 60, e.g., of the Belleville type, gripped between the body 48 and a jacket 62.
- This jacket 62 is fixed in the axial direction but is nonetheless able to rotate about the axis O. This rotation is provided by mounting the jacket 62 in ball bearings 64 and sealing rings 66, 76.
- the action of the spring 60 is therefore exerted on the body 48 and the sleeve 46, in the direction of the friction ring 58.
- the longitudinal movement of the body 48 is rendered independent of the jacket 62 and the angular movements between these components are rendered dependent by any known means, e.g., a pin 68 such as shown in the diagram.
- the rotation of the jacket 62 may be effected by means of a handle 70, whereby the rotation of the movable sleeve 46 and the masking of the slots 54 and 56 will vary by a greater or smaller extent, as explained with reference to the preceeding FIGURES.
- the pressure of the spring 60 is adjustable, e.g., by means of a regulating rod 72 and a securing nut 74.
- the aperture 24 may have an oval shape instead of a circular shape.
- the compressed air should preferably be admitted via channels or interstices 78 in the chamber containing the spring 60.
- the present invention provides an improved and novel device for injecting solid fuels (i.e., carbonaceous materials) into a shaft furnace.
- solid fuels i.e., carbonaceous materials
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Metallurgy (AREA)
- Fluid Mechanics (AREA)
- Combustion & Propulsion (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Materials Engineering (AREA)
- General Physics & Mathematics (AREA)
- Organic Chemistry (AREA)
- Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)
- Nozzles (AREA)
- Furnace Charging Or Discharging (AREA)
- Crucibles And Fluidized-Bed Furnaces (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| LU84462 | 1982-11-10 | ||
| LU84462A LU84462A1 (fr) | 1982-11-10 | 1982-11-10 | Dispositif d'introduction de quantites dosees de matieres pulverulentes dans un fluide de propulsion pneumatique et application a l'injection de combustibles solides dans un four a cuve |
| LU84812A LU84812A7 (fr) | 1983-05-19 | 1983-05-19 | Dispositif d'introduction de quantites dosees de matieres pulverulentes dans un fluide de propulsion pneumatique et application a l'injection de combustibles solides dans un four a cuve |
| LU84812 | 1983-05-19 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US4606677A true US4606677A (en) | 1986-08-19 |
Family
ID=26640293
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US06/550,565 Expired - Fee Related US4606677A (en) | 1982-11-10 | 1983-11-10 | Device for introducing dosed quantities of pulverized solid materials into a carrier gas stream |
Country Status (9)
| Country | Link |
|---|---|
| US (1) | US4606677A (fr) |
| EP (1) | EP0108319B1 (fr) |
| AR (1) | AR230884A1 (fr) |
| AU (1) | AU557972B2 (fr) |
| BR (1) | BR8306315A (fr) |
| CA (1) | CA1225418A (fr) |
| DE (1) | DE3375698D1 (fr) |
| ES (1) | ES526192A0 (fr) |
| PL (1) | PL137025B1 (fr) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5211751A (en) * | 1992-02-28 | 1993-05-18 | W.R. Grace & Co.-Conn. | Hydraulic cement set-accelerating admixtures incorporating amino acid derivatives |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| LU84780A1 (fr) * | 1983-04-28 | 1984-11-28 | Wurth Paul Sa | Dispositif d'introduction de quantites dosees de matieres pulverulentes dans un fluide de propulsion pneumatique et application a un reservoir de distribution de matieres pulverulentes |
| LU85299A1 (fr) * | 1984-04-11 | 1985-11-27 | Wurth Paul Sa | Dispositif d'introduction de quantites dosees de matieres pulverulentes dans un fluide de propulsion pneumatique |
| LU85298A1 (fr) * | 1984-04-11 | 1985-11-27 | Wurth Paul Sa | Dispositif d'introduction de quantites dosees de matieres pulverulentes dans un fluide de propulsion pneumatique |
| DE3436624A1 (de) * | 1984-10-05 | 1986-04-10 | Norddeutsche Affinerie AG, 2000 Hamburg | Vorrichtung zur erzeugung zuendfaehiger feststoff/gas-suspensionen |
| DE3507973A1 (de) * | 1985-03-06 | 1986-09-18 | Klöckner CRA Technologie GmbH, 4100 Duisburg | Dosierschieber fuer feinkoernige feststoffe |
| LU86311A1 (fr) * | 1986-02-19 | |||
| LU86870A1 (fr) * | 1987-05-07 | 1989-01-19 | Wurth Paul Sa | Dispositif de modification de la section d'une conduite de transport pneumatique et application a l'injection de combustibles solides dans un four a cuve |
| CN105712084A (zh) * | 2016-02-01 | 2016-06-29 | 北京理工大学 | 一种气体压力驱动式均匀供粉装置和方法 |
| CN111809033A (zh) * | 2020-07-22 | 2020-10-23 | 赣州市合安科技有限公司 | 一种进出料方便的井式回火炉 |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2731302A (en) * | 1953-05-11 | 1956-01-17 | Upham Charles Roland | Air switch and ported control head for powdered iron dispenser |
| US3006512A (en) * | 1958-07-16 | 1961-10-31 | Keathley | Material dispensing machine |
| US3527503A (en) * | 1968-08-05 | 1970-09-08 | Pullman Inc | Pneumatic outlet assembly for hoppers |
| SU371147A1 (ru) * | 1970-06-16 | 1973-02-22 | Н. И. Чебыкин, А. Н. Стриганов , И. Б. Левицкий Производственно техническое объединение Уралэнергоцветмет | Питатель всасывающей пневмотранспортной |
| US3840158A (en) * | 1972-10-17 | 1974-10-08 | Nordson Corp | Modular applicator system |
| GB1493525A (en) * | 1976-04-13 | 1977-11-30 | Lister & Co Ltd R | Agricultural broadcaster |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1094112A (en) * | 1964-10-14 | 1967-12-06 | Tills Engineering Co Ltd | Transporting and dispensing installation for granular and pulverulent material |
| DE2552594B2 (de) * | 1975-11-24 | 1977-09-22 | Ingenieurgesellschaft Industriebau mbH, 2000 Hamburg | Vorrichtung zum dosieren und absperren von staubfoermigen und rieselfaehigen schuettguetern |
| JPS5942045B2 (ja) * | 1980-05-22 | 1984-10-12 | ドネツキイ ナウチノ−イスレドバテルスキイ インステイチユ−トチエルノイ メタルルギイ | 微粉砕石炭を高炉炉床に供給するための通気供給器 |
-
1983
- 1983-09-28 AU AU19661/83A patent/AU557972B2/en not_active Ceased
- 1983-10-01 ES ES526192A patent/ES526192A0/es active Granted
- 1983-10-11 AR AR294508A patent/AR230884A1/es active
- 1983-10-24 EP EP83110587A patent/EP0108319B1/fr not_active Expired
- 1983-10-24 DE DE8383110587T patent/DE3375698D1/de not_active Expired
- 1983-10-28 CA CA000439963A patent/CA1225418A/fr not_active Expired
- 1983-11-10 BR BR8306315A patent/BR8306315A/pt not_active IP Right Cessation
- 1983-11-10 PL PL1983244498A patent/PL137025B1/pl unknown
- 1983-11-10 US US06/550,565 patent/US4606677A/en not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2731302A (en) * | 1953-05-11 | 1956-01-17 | Upham Charles Roland | Air switch and ported control head for powdered iron dispenser |
| US3006512A (en) * | 1958-07-16 | 1961-10-31 | Keathley | Material dispensing machine |
| US3527503A (en) * | 1968-08-05 | 1970-09-08 | Pullman Inc | Pneumatic outlet assembly for hoppers |
| SU371147A1 (ru) * | 1970-06-16 | 1973-02-22 | Н. И. Чебыкин, А. Н. Стриганов , И. Б. Левицкий Производственно техническое объединение Уралэнергоцветмет | Питатель всасывающей пневмотранспортной |
| US3840158A (en) * | 1972-10-17 | 1974-10-08 | Nordson Corp | Modular applicator system |
| GB1493525A (en) * | 1976-04-13 | 1977-11-30 | Lister & Co Ltd R | Agricultural broadcaster |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5211751A (en) * | 1992-02-28 | 1993-05-18 | W.R. Grace & Co.-Conn. | Hydraulic cement set-accelerating admixtures incorporating amino acid derivatives |
Also Published As
| Publication number | Publication date |
|---|---|
| AR230884A1 (es) | 1984-07-31 |
| AU557972B2 (en) | 1987-01-15 |
| ES8406696A1 (es) | 1984-08-16 |
| AU1966183A (en) | 1984-05-17 |
| CA1225418A (fr) | 1987-08-11 |
| EP0108319A2 (fr) | 1984-05-16 |
| DE3375698D1 (en) | 1988-03-24 |
| EP0108319B1 (fr) | 1988-02-17 |
| PL137025B1 (en) | 1986-04-30 |
| ES526192A0 (es) | 1984-08-16 |
| PL244498A1 (en) | 1984-07-16 |
| BR8306315A (pt) | 1984-06-19 |
| EP0108319A3 (en) | 1985-11-21 |
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